Bill3752
Chemical
- Jan 24, 2008
- 138
We recently sized a relief valve for steam service. The vendor (Crosby) rep recommended an HSJ conventional valve (2 1/2 K 4). I did some quick calcs and critical flow is computed, even with discharge to atmosphere; with a small bit of tailpipe and an elbow, the dP is much greater than 10%.
Two questions:
1. Does it make sense for a manufacturer to design a valve, such that there is choked flow at the discharge?
2. I was told, but cannot confirm, that the dP must be limited to 3% for an ASME Code Section I valve. It that is the case, I don't believe we could achieve this without a very large RV outlet flange.
I suspect I am missing something here. Any thoughts?
Two questions:
1. Does it make sense for a manufacturer to design a valve, such that there is choked flow at the discharge?
2. I was told, but cannot confirm, that the dP must be limited to 3% for an ASME Code Section I valve. It that is the case, I don't believe we could achieve this without a very large RV outlet flange.
I suspect I am missing something here. Any thoughts?